Competition of bloom-forming marine phytoplankton at low nutrient concentrations

Competition of three bloom-forming marine phytoplankton (diatom Skeletonema costatum, and dinoflagellates Prorocentrum minimum and Alexandrium tamarense) was studied through a series of multispecies cultures with di erent nitrate (NaNO3) and phosphate (NaH2PO4) levels and excess silicate to interpret red tide algae succession. S. costatum outgrew the other two dinoflagellates in nitrate and phosphate replete cultures with 10 mol/L Na2SiO3. Under nitrate limited (8.82 mol/L NaNO3) conditions, the growth of S. costatum was also dominant when phosphate concentrations were from 3.6 to 108 mol/L. Cell density of the two dinoflagellates only increased slightly, to less than 400 and 600 cells/mL, respectively. Cell density of S. costatum decreased with time before day 12, and then increased to 4000 cells/mL (1.5 mg/L dry biomass) at NaNO3 concentrations between 88.2 and 882 mol/L with limited phosphate (0.36 mol/L NaH2PO4) levels. In addition, P. minimum grew well with a maximal cell density of 1690–2100 cells/mL (0.5–0.6 mg/L dry biomass). Although S. costatum initially grew fast, its cell density decreased quickly with time later in the growth phase and the two dinoflagellates were dominant under the nitrate-limited and high nitrate conditions with limited phosphate. These results indicated that the diatom was a poor competitor compared to the two dinoflagellates under limited phosphate; however, it grew well under limited nitrate when growth of the dinoflagellates was near detection limits.     

Removal of phosphate by Fe-coordinated amino-functionalized 3D mesoporous silicates hybrid materials

Phosphate removal from aqueous waste streams is an important approach to control the eutrophication downstream bodies of water. A Fe(III) coordinated amino-functionalized silicate adsorbent for phosphate adsorption was synthesized by a post-grafting and metal cation incorporation process. The surface structure of the adsorbent was characterized by X-ray di raction, N2 adsoropion/desoprotion technique, and Fourier transform infrared spectroscopy. The experimental results showed that the adsorption equilibrium data were well fitted to the Langmuir equation. The maximum adsorption capacity of the modified silicate material was 51.8 mg/g. The kinetic data from the adsorption of phosphate were fitted to pseudo second-order model. The phosphate adsorption was highly pH dependent and the relatively high removal of phosphate fell within the pH range 3.0–6.0. The coexistence of other anions in solutions has an adverse e ect on phosphate adsorption; a decrease in adsorption capacity followed the order of exogenous anions: F?? > SO2?? 4 > NO??3 > Cl??. In addition, the adsorbed phosphate could be desorbed by NaOH solutions. This silicate adsorbent with a large adsorption capacity and relatively high selectivity could be utilized for the removal of phosphate from aqueous waste streams or in aquatic environment.     

Modeling assessment for ammonium nitrogen recovery from wastewater by chemical precipitation

Chemical precipitation to form magnesium ammonium phosphate (MAP) is an effective technology for recovering ammonium nitrogen (NH4 +-N). In the present research, we investigated the thermodynamic modeling of the PHREEQC program for NH4 +-N recovery to evaluate the effect of reaction factors on MAP precipitation. The case study of NH4 +-N recovery from coking wastewater was conducted to provide a comparison. Response surface methodology (RSM) was applied to assist in understanding the relative significance of reaction factors and the interactive effects of solution conditions. Thermodynamic modeling indicated that the saturation index (SI) of MAP followed a polynomial function of pH. The SI of MAP increased logarithmically with the Mg2+/NH4 + molar ratio (Mg/N) and the initial NH4 +-N concentration (CN), respectively, while it decreased with an increase in Ca2+/NH4 + and CO3 2??/NH4 + molar ratios (Ca/N and CO3 2??/N), respectively. The trends for NH4 +-N removal at different pH and Mg/N levels were similar to the thermodynamic modeling predictions. The RSM analysis indicated that the factors including pH, Mg/N, CN, Ca/N, (Mg/N) (CO3 2??/N), (pH)2, (Mg/N)2, and (CN)2 were significant. Response surface plots were useful for understanding the interaction effects on NH4 +-N recovery.     

无砾石微孔管地下渗滤系统试验研究

针对传统无砾石管式地下渗滤系统存在的处理性能差,渗滤通量低两个问题,通过去掉包裹织物,提高渗滤管开孔率、改变开孔方式,设计了无砾石微孔管地下渗滤系统。通过实验研究表明,无砾石微孔管地下渗滤系统对COD、氨氮的去除率比传统管式系统分别提高了10.8%、12.7%,总磷去除率并无显著差异,ORP值提高约85 mV,渗滤通量提高26.8%。在3.3 cm/d的水力负荷下,无砾石微孔管地下渗滤系统出水COD、氨氮、总磷平均浓度分别为19 mg/L,0.62 mg/L,0.048 mg/L。渗滤管下10 cm的土壤层去除了约70%的COD,80%的氨氮和91%的总磷,向下随着土壤深度的增加,单位厚度的土壤层去除的污染物量呈显著下降趋势。     

吸附剂烟气脱砷的研究现状

大气砷污染问题日益引起人们的重视,吸附剂能够在去除烟气中砷的同时去除其他有害气体,是控制烟气砷含量、防止砷污染的有效途径.文章分析了砷在废气中的形态及分布,总结了近年来氧化钙、活性炭、飞灰和金属氧化物作为吸附剂用于烟气脱砷的最新研究进展,重点分析了各自的吸附机理及不同因素对脱砷过程的影响.指出吸附过程通常以化学吸附为主...     

免烧粉煤灰陶粒作为BAF填料处理城市污水

以电厂粉煤灰为主要试验原料,辅以外加药剂(水泥、石灰、石膏、水玻璃),经混合、成球、陈化和养护等工序,制得免烧粉煤灰陶粒,并将其作为曝气生物滤池(BAF)工艺的载体填料处理城市污水.待挂膜启动成功后,考察了水力停留时间( HRT)、COD负荷、氨氮负荷对COD和氨氮去除效果的影响.实验结果表明:在温度为18～21℃、气...     

不同进水条件对SBR工艺脱氮除磷效能的影响

采用人工配水,研究进水在不同pH值,碳源类型,碳氮比条件下,厌氧/好氧/缺氧(A/O/A)sBR工艺对生物法脱氮除磷效能的影响.结果表明:不同的进水条件对反应器的影响较大,当pH值为7.5,乙酸钠为碳源,碳氮比为1.4时,反应器运行效果最佳,系统对PO43--P,NH4+-N的去除率分别达到97.28%,99.5%.N...     

刘家峡水库水环境质量生物学评价研究

2008年黄河丰水期和2009年黄河枯水期,对研究区6处标志性区域进行随机采样,采用活体观察和固定染色法鉴定藻类种类,直接计数法统计藻类数量,共鉴定到藻类114种(包括22个未定名物种),隶属于9门11纲17目34科55属。其中,硅藻门47种,占41.22%,以无壳缝目为优势类群;绿藻门24种,占21.05%,为次优势类群;蓝藻门,金藻门,裸藻门为常见类群;隐藻门、甲藻门和黄藻门均为罕见类群。利用藻类群落结构特征、优势种类、藻类污染指数和污生指数等指标对刘家峡水库水质进行评价,结果表明:刘家峡水库水质在1#、2#样区较清洁,3#、4#样区为轻-中度污染,5#、6#样区为重度污染,与采用粪大肠肝菌、DO指标评价结果具有良好一致性。     

北方某钢铁厂部分厂区土壤重金属污染的初步调查

对北方某即将搬迁钢铁厂的部分厂区土壤重金属进行了初步调查,主要利用SPSS相关和变异分析、Surfer空间分析及归一化处理对重金属污染的空间分布特征进行了描述。一区污染最为严重,有Hg、Mn、Zn、As、Cr和Cu;二区污染物主要为As、Pb和Zn;三区污染主要有As、Cr和Co;四区污染物有Cr、Co、Mn、Cu和Pb,污染相对较低。研究为调查区域搬迁后的土地规划提供了科学依据。     

诱导结晶磷回收技术处理低浓度含磷废水研究

诱导结晶技术是近年发展的新型废水处理技术。采用自设计的诱导结晶反应器,反应器形式与Phosnix相似,但结构相对简单,无Phosnix反应器的内外同心筒结构,并增加了过渡区。研究了HRT、[PO43-]、[Ca2+]/[PO43-]对诱导结晶处理低浓度含磷废水的影响规律,并以实验室双泥系统厌氧上清液为原水,考察了结晶反应器长期运行效果。研究表明,在一定范围增加HRT、[PO43-]或[Ca2+]/[PO43-]均可提高磷酸盐去除率,但超过一定数值后,再继续增加对提高磷酸盐去除效果的贡献很小,[PO43-]或[Ca2+]/[PO43-]过高还会导致均相结晶出现,使磷酸盐去除率下降;研究给出了一定条件下的最佳HRT、[PO43-]或[Ca2+]/[PO43-];运行效果试验表明,诱导结晶反应器在进水平均磷酸盐浓度仅为23.6 mg/L的情况下,磷酸盐的平均去除率仍可达到55.2%,该技术在处理低浓度含磷水方面较具应用前景。